Air-liquefier.



JAMES F. PLACE, OF GLENRIDGE, NEW JERSEY, ASSIGNOR-'IO AMERICAN AIR LIQUEFYIN G CO., A CORPORATION OF NEW YORK.

manzoni-irma.

Specification of Letters Patent.

Patented July 13, 1909.

Application filed. September 11, 1906. Serial No. 334,104.

To all whom it may concern:

Be it known that I, JAMES F. PLACE, a citizen of the United States, and a resident of Glenridge, in the eountv of Essex and State of New Jersey, have invented certain new and useful Improvements in Air-Liqueiers, of which the following is a specification. My invention relates to improvements in apparatus for liquefying atmospheric air.

The object is to produce liquid air at less expenditure of energy than heretofore, and thereby reduce tlic cost of its production. I attain this object in the manner herein described and as illustrated by the accompanying drawings, in which- Figure 1 is a vertical section, showing the liqueer and other accessories connected therewith. Fig. 2 is a diagrammatic drawing showing the necessary mechanism and connection for compressingl cooling and drying the air previous to its admission to the counter-current coils and the liqueiier.

Similar reference marks refer to similar' parts throughout the several drawings.

At the numeral 1 in Fig. 2, I show an ordinary air compressor, shown preferably as a two-stage compressor, having the low-pressure cylinder 2 and the high-pressure cylinder 3 with the inter-cooler l between. At 5 isshown a wheel to which power may be connected by belt. At 6 is shown an ordinary wat c1'-eooler for removing the heat of compression.

It is very necessary in liquefying air that all moisture in the air be removed, otherwise frost and ice will form in and clog the pipes. So also must the carboiiie acid gas be removed from the air. otherwise it remains not only to clog thc pipes but comes out with the liquefied air in form of frozen liquid carbon dioxid; and oftentimes in such quantities as to be troublesome to remove.

use referably calcium ehlorid to remove a portion of the moisture from the air, and

then caustic potash to remove more moisturc and to also absorb the carbonio acid gas (CO2) from the air. I then subject the air to a freezing process by mechanical re.

frigeration, to freeze out any remaining moisture which may be in it. In my experienee I find that the calcium clilorid and caustic potash, if the drums are properly constructed, will take air at ordinary saturation of 7 5% or higher, and reduce tlie moisture to 14% saturation. This method of removing moisture and CO2 from the air is not new, but some of the appliances for doing the work are new and their novel construction is new, Letters Patent for which I have made application.

I show my calcium chlorid moisture extractor at 7, in form of a vertical drum charged with lump calcium chlorid, the air entering same through the pipe S from the cooler 6, and passing out of the drum through the pipe 9. Thence it enters a similar drum 10, which is charged with caustic otash in the lump. After thus being c emically dried and the CO2 gas being absorbed by the caustic potash, I pass the air through the pipe 11 to a rcfrigerating drum 12. This drum (12) is of novel construction inside. The refrigeration is produced in the usual manner, either with ammonia or carbon dioxid, preferably the latter. I show at 13 a CO2 gas compressor (power being supplied thereto by belting to the wheel 13') which discharges into the water cooling condenser 14 through the connecting pipe 15.

The highly compressed COz gas is condenscd to a liquid in the condenser 14, which drops by gravity into the liquid holding'taiik 16. From thence the liquid CO2 is conducted through the pipe 17 to the pressure releasing or expansion valve 1S. It passes through a copper coil in the drum 12, in counter-current to the compressed air delivered from the pipe 11. The CO2 li uid released from ressure evaporates in t ie co8- per coils, am the gas is delivered to the C 2 compressor again through the pipe 19, and is re-compressed and condensedA as before. A temperature of '-30 to l0 F. can easily be obtained in this way, and the remaining moisture in the compressed air will be deposited on the CO2 copper coils in the drum 12, and subs xiently melted and drained olf through the lip cock 20. The air is now ready for liquefying, and is delivered to the thermal interchanger and my improved submerged liquefier or high-pressure air-liqueying condenser, hereinafter described.

The usual method of liquefying air, is to utilize the cooling effect produced by what is known as the tlirottled nozzle and countercurrent thermal interchanger system. Air is compressed to a high tension (to 100 and often to 200 atmospheres), and then released, often to atmospheric pressure. In this way the Joule-T iempson effect, so

before expansiomin centigrade.`

- tion.

called, is utilized, in accordance with the well-known formula: Px lp: the

fall in temperature in centigrade degrees; wherein Il 1s the pressure in atmospheres before ex ansion, l?2 the pressure after ex pansion, and the absolute temperature of the air The cooling effect obtained bv expanding air through a throttled nozzle rom a constant relatively high to a constant relatively low pressure, is about half a degree Fah. per each atmosphere released-increasing somewhat as the initial temperature falls and the initial pressure is increased. After release, the low pressure air is carried back in a counter-current thermal interchanger over the highressure airsupply pipes, further reducing t te temperature of the initial air before release by the nozzle, and thus producing a cumulative fall in temperature of the released air, until the Vtemperature of lquefaction for air at the lower pressure is reached, when about 7 of vthe air liqueiies; the latent heat of condensation given out and the reduction in quantity of the gaseous air carried back for cooling the incoming high-pressure su iply, neutralizes any higher percentage o Liquefac- Another and older method is that of en'panding the air in an insulated airex anston engine, and using the exhaust au' rom the engine by a similar counter-current thermal interchanger to cool the compressed air supplied to the same. This method gives a very much greater fall of temperature per atmosphere expanded; and therefore not nearl f so great an mitral compression 1s require wluch assures a very considerable saving in energ besides the recovery of the power obtained from the expansion engine. Both of the foregoing methods are now in practical use. My present invention; however, 1s based on a different method from either of the foregoing. I utilize the latent heat of vaporizatiomrequired by liquid air at substantially atmospheric ressure, to cool and liquey air while at or a ove its critical pressure when there is no latent heat of condensation given out to neutralize refrigeration and retard liquefaction. It is well known that the critical pressure of air is 39 atmospheres, and its critical temperature is -220' It will condense to a liquid at -220 F., l

if it be compressed to 39 atmospheres; and it will liquefy at a lower compression if cooled to a lower tem eraturc, or at atmospheric pressure if cooed to 312.6 F.; but no amount of compression will cause liquefaction unless it be cooled to its critical temperature, namely, 220 F. If compressed to 39 atmospheres and cooled to -220 F., its density then as a gas is identical with its density as a liquid; and with the slightest lowermg of the temperature then, its change of state from a gas to a liquid (if the pressure is maintained) is instantaneous, and there can be no latent heat of condensation, as there is practically no further contraction.

By my system I compress air to about 45 atmospheres (647 lbs. gage) and liquefy all of the air compressed, without any reduction of pressure. It is liquefied in a highpressure condenser, which is kept submerged in liquefied air of substantially atmospheric pressure, and after liquefaction it is sub-cooled as a li uid before release from pressure, until it is zilnout the same temperature of the low-pressure liquid air surrounding the condenser, or 313 F. Afterward it is released from pressure (as a subcooled liquid) and delivered to the insulated reservoir which surrounds the condenser, (thus rcplenishing the evaporating liquidcharge therein) to liquefy and sub-cool new and successive charges of cooled compressed air in the submerged condenser. The latent heat of vaporization required by liquid air at atmospheric pressure 1s about 120 B. t. u. per pound; and this, with the cooling effect of the vapor of the evaporated liquid (as it passes through the thermal interchanger and absorbs heat from the incoming compressed air until it rises from 313 F. to normal temperature), is all utilized. In this way a large saving is made in power, for any compression above 45 atmospheres would be practically a waste of energy; and every pound of liquid air evaporated at atmospheric pressure will cool and liquefy about double the quantity of air compressed to or a trifle above the critical pressure (39 atmos heres), leaving liquefied about 50% of all t ie air compressed as the net output in liquid air, or the net product of the apparatus for outside or commercial uses. This system and my ar-liquefying apparatus I will now proceed to describe.

Having thoroughly dried the compressed air and removed therefrom the COz gas, I deliver the same to the counter-current cooling coils and liquefier, shown in Fig. 1, comprising for the high-pressure, one or more copper pipes 22 of suitable length, which carry the compressed air in (as received from the supply pipe 23, shown in Figs. 1 and 2) to the h ueiier. These pipes 22 are in form of helica coils inclosed by the non-conducting insulated drumor longitudinal double walled conduit 24 and 24'. The center of this helical coil (22) is lled'by the core or drum 25. By the construction shown, there is provided a low-pressure return passage 40, between the coils 22, within the conduit or drum 24, helically around the core 25, up,

I 25 the inlet to said valve 927,594 y QB" lower end, which has an enlarged part, or the liqueiier pro er 27, made of copper, extending still fart er down. This lower end 27, or air-liquefying condenser is inelosed by the liquid air holder 28, having a vacuum jacket 29 inclosin the vacuum 30 around the holder 2S. .girlie holder 2S is the lower end of the low-pressure conduit 24, and is made of suitable impervious metal of low thermal 1o conductivity. The condenser 27 is kept constantly supplied with cooled comylressed air from the pipes 22, at substantia y the crit-ical pressure; and this pressure is maintained in the condenser at all times. At 31 I show a liquid-discharging overfiow outlet for the liquid air holder 28, regulated by the valve 32, which is operated by the long insulated non-conducting stem 33, and han wheel 34. rl`his overflow or outlet pipe is so arranged that it can be turned upward as shown by the dotted line 35, an( used to charge the holder 28 with an initial charge of liquid air, in starting up.

At 41 I have a liquid discharging valve, being in form of a siphon 42, which extends to near the bottom inside of the submerged condenser 27, or so located that only liquefied air can be delivered from the condenser '27 to and through said 30 liquid discharging valve 41. This liquid discharging valve delivers directly into the liquid air holder 2S, through the downwardly extended discharge pi e 43. Valve 41 1s operated by means of t 1e hand wheel 44 and non-conducting insulated stem 45. At 46 I have an inlet to the vacuum space 30, to which an air pump may be attached. After producing a vacuum in 3G, I ill the vacuum space with carbonio acid gas under slight pressure, and then seal with the soldered cap 47. Within the wire gauze 48 or 4S', I put charcoal, to absorb any air which may e in the CO2 gas; this charcoal is held by the gauze 4S in contact with the surface of the bottom of the holder 2S, where the temperature is constantl)r very low; at extremely low temperatures charcoal has great ewer of absorbing air. On charging the vessel 2S through t ie pipe 35 with an initial I 50 charge of liquid air, the CO,gas in the space 30 will quickly condense and be deposited as COz frost on the coldest surface of the vessel or holder 2S, thus reducing a. high vacuum in said space an surround@ t e lir uid air in said vessel with the best possillilc insulation. .-lt 2S I show a cup-shape catch fixed around the bottom of the vessel 2S, within the vacuum space 30, which is for the purpose of catching or holding any l liquid C()2 which may drip down on the surface of the vessel 2S, thus holdin r said li uid COz close to the cold surface of t 1e vesse 28 so as to prevent itrevaporating to a gas.

The space between the walls of the low pressure conduit 24 and 24 may be filled with cider-down or other suitable insulator; and the whole may be packed in hair felt 49, or some other suitable insulating packing, and inclosed by the non-conductingbarrel 50.

The ex anded or return fiow of air leaves the intere anger by the pipe or conduit 51, and may be returned to the com ressor and re-compressed, by closing the va ves 52 and 53, (see Fig. 2) and opening valve 54; or b closing 53 and 54 and opening valve 52, 1t 75 will be discharged to the open air.

An im ortant and novel feature of my invention is the location of the liquefier proper or high-pressure condenser 27, within the liquid air vessel or holder 28; and making of 80 that condenser a closed drum, as it were, so that only compressed air of hivh tension (to or above itsl critical pressure fills it, and without current or flow therein, as all the air suglplied to it becomes liqueiied; thcre 85 fore t e only deliverv of compressed air thereto is to take the place of that which has become liquefied therein while at substan tially its critical pressure; and no air can esca e therefrom until after it is liquetied. By aving this condenser 27, located as shown, it is submerged in the liquid air in the vessel or holder 2S, at all times, whether the holder has therein an initial charge of liquid air, or whether it is supplied with liquefied air from the condenser 27. The liquefied air as it accumulates in the condenser or liquefier 27, may be discharged through the liquid discharging valve 41 in separate and distinct charges, intermittently, or it ma be discharged continuously before it entire fills the condenser 27.

It during the operation of the ap aratus valve 52 (see Fig. 2) is kept open an valves 53 and 54 are ke t closed, my apparatus -in 105 liqueying will a so partially separate the two gases, oxygen and nitrogen, (owing to the diiferenco in temperature of their boiling points) by fractional distillation in evaporating'principally the nitrogen of the lique- 110 ied air in the low-pressure holder 2S; and consequently the overiiow liquid drawn from the apparatus through discharge tube 31 will be veryrich in oxygen, and the re turn flow of expanded gas or air leaving the system through valve 52 will be correspondingly rich in nitrogen.

At 36 I show an airexpansion valve, generally'for use only in starting up, when an initial charge of liquid air for the evaporating vessel 21 is not obtainable; i't is located above the condenser 27, or between it and 'the compressed-air supply. By opening this valve (36) a trifle, it acts as a tlirottled orifice or porous plug, and the com rcssed air in pipes 22, (at 45 to 50 atmosp eres tension) is released or let down to substantially atmospheric pressure after it has passed through said valve; and in thus being released it drops 1n temperature in accordance 130 1 n saws i opening of the valve 36 not being so great as to reduce the pressure. As soon as the holder 2Q is filled with a liquid-air charge,

valve 36 may be closed and its further use dis )ensed with, it preferred.

f the liquefied air in the high-pressure condenser 27 is discharged therefrom as soon as condensed, then the latent heat of vaporization required, as released from ressure, would naturally be absorbed from t 1e li uid itself, until its temperature falls to its boi ing point 313 l". The preferred method of o ierating, however, is to allow the li uefied an' in the higlbpressure subincrgei condenser .7 to remain therein until 1t is subcooled, or cooled after liquefaction, down from 220 F., to 4312.6" F., the temperature of the liquid air surrounding the condenser in the insulated evaporating vessel 2S. Then the liquid air in the condenser '27 as released from pressure and delivered to the evaporatiug vessel 28, will already be at -3l2.6 1"., and will not vaporize on being released. Evaporation, or fractional distillation of the liquid in the holder 2S `will then go on continuously, for the diflerence in temperature between the ex-aporating liquid au' in the holder 2S and the liquefying point of the cooled compressed air (40 to 45 atmospheres) in the condenser '27, is 03 degrees rahrenheit; the latent heat, now at its maximum, being drawn entirely from both the cooled compressed air and the liquefied air in the condenser 2T-rapidly liquefying the compressed air therein (without. reduction of pressure) and sub-cooling the liquid as fast as produced. All of the vapor from the evaporated liquid air in the holt er 12S, atsubstantially atmospheric pressure. andat a temperature `when evaporated of -Rll F., is carried back in the conduit '24, through the passage 40, and serves to cool the incoming supply of compressed air in the counter-current coils 22.

An important feature of the system is the fact thatthe evaporating holder or insulated reservoir 2S cannot be emptied: once charged it remains pmctieallv full of liquid air at substantially atmospheric pressure. during the operation of the apparatus. the surplus, or overllou alone being drawn from the reservoir. This surplus or output of liquid air, bv reason of the high-pressure submerged liqueier herein shown. and other valuable features herein described, will be much more than heretofore obtained for the energy expended in this class of air-liquefying apparatus, or about 50% of all the air treated. Iaving thus described my invention, what -with said container-arranged I claim as new and original and desire to secure by Letters Patent, is-

1. An apparatus for liqueying air, comprising in o rati-ve combination a liquefier; a liquid-air holder; and two discharging valves, delivering to said holder-one a compressed-air expansion valve, and other a liquefied air discharging valve leadu ing from the liqueiier; said liqueiier being arranged to be submerged in tie li uid air produced or liqueed in said lque er anl delivered to said holder.

.Anapparatus for liquefying air, comprismg 1n onerative combination a ig pressure air-liquefying conduit; a lo\vressure liquid-air evaporating conduit; an two pressure-releasing discharging valves-one a compressed air expansion valve, arranged to release from pressure and discharge only com pressed air to said low-pressure liquid-air evaporating conduit, and the other a liquidair valve, arranged to release from pressure and discharge air after it is liquefied, and from said high-pressure to said low-pressure conduit.

3. An apparatus for liquefying air, comprising in operative combination, a liquid-air evaporating inclosure; and air-liquefying condenser within said inclosure; and two pressurc-releasing discharging valves-one a compressed-air expansion valve, arranged to release from pressure and discharge only compressed air, and the other a liquid-air valve, arranged t-o discharge air after it is liquclied; and both of said valves arranged to discharge from the same relatively high to the same relatively'low pressure, and deliver to said evaporating inclosure.

4. An apparatus for liquefying air, comprising in operative combination,` a liquidair evaporating inclosure; two pressurereleasing discharging valvesone a compressed-air expansion valve, arranged to release from pressure only and discharge thereafter' compressed air, and the other a liquid air valve, arranged to discharge air after it is liquefied both of said valves being arranged to discharge from the same relatively high to' the same relatively lou' pressure, and closure; and a high-pressure air-liquefying condenser adapted to be submerged in the low-pressure liqueed air in said 'evaporating inclosure.

5. An apparatus for liquefying air consisting of one or more high-pressure pipes, and a low-pressure conduit inclosing the same having a liquid-air evaporating container; means for supplying compressed air to the system at one end of said pipe or pipes; and a high-pressure liquefying condenser at the other end, having a liquid-air discharging valve connecting said condenser to be submerged in the liquid air previously produced deliver to said evaporating m the therein; and an air-expansion or pressurereleasing air valve connected with said highpressure pipe, between said condenser and said compressed-air supply -said valve being arranged to release from pressure and deliver air from said high-pressure pipe to said lowpressure conduit.

6. An apparatus for liquefying air, comprising in operative combination, a countercurrent system, consisting of one or more inwardly delivering com ressed air pipes, longitudinally inc osed y an outwardly delivering expanded-air conduit opening to the atmos here, having at its lower end an insulated iquid-air evaporating holder, provided with an overflow outlet, and arranged to hold liqueed air without loss except by evaporation or overflow therefrom; and a high-'pressure liqueiier within said evaporatiug holder, provided with an adjustable va ve which connects said liqueiier with said holder-said liqueiicr being connected with the inwardly delivering end of said compressed air pipe or pipes.

, 7. An apparatus for liquefying air, comprising in operative combination, a countercurrent system consisting of one or more inwardly delivering compressed-air supply pipes longitudinally inclosed by an outwardly delivering ex anded-air conduit, having at its lower or ii et end an insulated liquid air receptacle or holder, provided with an overllow outlet delivering outside the system; and a high-pressure liquefier within said liquid air holder, irovided with an adjustable liquid-air discliargeing valve, the upper eiid of said liqueiicr being 'lived to and connected with the inwardly delivering end of said com ressed air supply pi es, and its lower en( being connected wit i said insulated liquid-air receptacle, through said adinstable liquid air valve.

8. An apparatus for liquefying air, comprising in operative combination a countercurrent system of one or more inwardly-delivering com ressed-air supply pi es, longitudinally inc osed by an outward '-delivering low-pressure expanded-air conduit, vented to the atmosphere, rovided at its lower or inlet end with an insulated liquid-air evaporating holder, having an overow outlet delivery outside the system; a high pressure condenser within said insunie liquid-iii holder, connected with said compressed air supply pipe or ipes; and means providing for withdrawal rom said high-pressure condenser of air after it is liquefied-the parts when in operation being so arranged that said condenser is constantly submerged in liquid air of substantially atmos herie pressure which was previously liquefied at relatively high compression and without reduction of pressure in said condenser.

An apparatus for liqueying air, comrising in operative, combination one or more high-pressure pi es, and a low-pressure conduit or casing longitudinally inclosing the samesaid conduit or casing having an in sulated liquid-air evaporating holder at its lower end; means for sup lying compressed air to one'end of said higli pipes, with the other end thereof, within said evaporating holder; and an air-expansion valve between said liquefier and said means for supplying compressed air, arranged to deliver air from the high-pressure pipe or pipes to said low-pressure conduit, and expand the same therein.

10. An apparatus for liquefying air, comprisin in operative combination, one or more high-pressure pipes, and a low-pressure conduit or casing longitudinally inclosing the same, vented to the atmosphere, and having at its lower end an insulated liquid-air evaporating holder arrangedto allow liquid air to be evaporated therein; means for supplying compressed air to the system at one end of said high-pressure pipe or pi es, and a highpressure liqucfier fixed to an connected with the other end, within said holder; and a liquid airdischarging valve connecting said highressure liqueiier with said low-pressure liqui -airevaporating holder.

11. An apparatus for liquefying air, comprising in operative combination, countercurrent high-pressure and low-pressure conduits-the rst longitudinally inclosed by thc last, and said low-pressure conduit havingan insulated liquid-air cvaporating holder at its'lower end; means for supplying compressedair to the system at one end of said igli-pressure conduit, and a high-pressure fixed to and connecte with the orating holder; and arranged to maintain t e air delivered thereto without reduction of pressure; an airexpansion valve between said liquelier and said com ressed supply, arranged to deliver air rom said high-pressure to said lowpressure conduit and a liquid-air dischargingvalve Vconnecting said liqueier with said holder. "1

12. In an air-liquefying apparatus the combination with a counter-current 'ghpressure and low-pressure conduit; of an airexpansion valve for utilizing the Joule- Thomson eect-said valve being connected with and fed from said high-pressure conduitand delivering to said low-pressure conduit; a liquid-air evaporating holder connected with said low-pressure conduit; and a stillair high-pressure condenser, or extension of said highressure conduit beyond said expansion vzilve, provided with a liquid-air dislicueiier ot ier vend, within said eva charging or pressure-releasing valve-said extension or still-air condenser being arrangedto be submerged in the liquid air -piessure pipe or and a high-pressure lignei-ler connected` iio ` pressure-releasing valve.

' 13. In an liquefying apparatus theY combination with a counter-current high pressure and low pressure conduit, and an air expansion valve for utilizing the Joule- Thomson eiect; of a liquid-air evaporating holder connected with said low-pressure conduit; an air-liquefying high pressure condenser or extension of said high pressure conduit beyond said air ex ansion valve, and having a liquid air disc arging valve, said extension of the high pressure conduit or air liqlllefying condenser being arranged to be su merged in the liquid air as produced 1n the ap aratus,the arts being so arranged that a vapor causedpby evaporation of any portion of the successive low-pressure liquid air char es, passes into the low-pressure eenduit an helps to cool the compressed air being supplied to the apparatus;

14. A n apparatus for liquefying air, comprising an insulated 10W-pressure liquid-air evaporating vessel, and an air-liqueiying high-pressure condenser within the same; in O erative combination with means for supp ving said condenser with air compressed to substantially its critical pressure; and means providing for vreleasing from pressure and discharging from said condenser, to said holder, the air after it is liquefied therein-f said condenser beingarranged to be submerged in the low-pressure liquid air in said holder as released from pressure and delivered thereto from said condenser.

15. An apparatus for liquefving air, comolder, having an expan ed air or vapor conuit delivering therefrom; in Operative combination with a compressed-air supply pipe within said conduit, having an air-liquefying condenser at one end, in said holder; means 'Erisng a low-pressure liuld-air evaporating at the other end of said pipe for supplying" the same with air compressed to substantially its critical pressure; and means providing for releasing from pressure and discharging from said condenser to said holder, the air after it is liquefied in said condenser. 16. An air-liqueer comprising in operative combination, a low-pressure liquidair evaporating vessel, having an outwardly delivering expanded air or vapor conduit connected with and delivering therefrom; an in- Wardly delivering compressed-air pipe Within 5 said conduit, arranged to be submerged at its lower end in the evaporatin' liquid air in said vessel; and an adjustable Lliquid-air pressure-releasing discharging valve connected with the outlet end of said eompressed-air pipe, and releasing from pressure and delivering therefrom to said .evaporating vesselV the air after its is liquefied.

17. An apparatus for liqueying air, .com prising an insulated low-pressure liquid-air evaporating vessel, vented to the atmosphere; and an air-liquel'ying high-pressure condenser within the same; in operative eembination with means for supplying said condenser with air compressed to substantially its critical pressure; and means for releasing and delivering liquid air from said condenser to said evaporating vessel-Whereby portions of the same are evaporated at substan* tially atmospheric pressure in said vessel by T heat derived from air compressed substantlall to or above its critica con( enser; v

Signed at New York 1n the county of New Ork and State of New York this 23d day of 80 y Witnesses:

JOHN A. INsLnn, G. JOHNSON.

pressure in said Y 

